Filtering or straining or like treatment of fluids



June l1, 1940. n l

W. J. FRREST FILTERING on summa@ on uns 'rnEATuENT or muws Filed Aug. '26, 1937 8 Sheets-Sheet 1 oo J.. lllllfllll n 6 rif a lin 6 I 1i June 1l, 1940- w. J. FoREs FILTERING 0R STRAININGIOR LIKE TREATMENT 0F FLUIDS Filed VAug. 26, 1937 8 Sheets-Sheet 2 5| Q MIF l/ Arron/Ey W. J. FORREST FILTERING 0R STRAINING 0R LIKE TREATMENT 0F FLUIDS lJune ll, 1940.

Filed Aug. 26, 1937 8 Sheets-Sheet 3 Fig. 3.

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Junefll, 1940.` w L FORREST V 2,204,349

l FILTERING OR'STRAINING 0R LIKE TREATMENT 0F FLUIDS Filed Aug.,26, 1937 8 Sheets-Sheet ATTORNEY June 11, 1940. i w.- LVFORREST l 2,204,349

FILTERING OR STRAINING OR LIK TREATMENT OF'FLUIDS Filed Aug. 26, 1957 @sheets-sheet. 5

/TTOP/VEY June ll, 1940. w. J. FoRRl-:s'r-

FILTERING 0R STRAINING OR LIKE TREATMENT 0F FLUIDS Filed Aug. 26, 19s? 8 Sheets-Shale?l 6 MM@ v A 770/?NEY June ll, 1940. uw, FQRREs-r 2,204,349

FI`LTERING'OR STRA-INING 0R LIKE TREATMENT QF FLUIDS Filed Aug. 2e, 1937 8 Sheets-sheet '7 Arrbm/Ey June 1l, 1940. I w J, FQRRE'ST 2,204,349

l FILTERING 0R STRAINIHG OR LIKE TREATMENT OF FLUIDS l Filed Aug. 2e, 19.37 s sheetssheet s M/zw 7M A WORM/5y Patented June 11, 194@ l 2,204,349-H FILTERING on s'rRAINl-NG on LIKE TREATMENT oF FLUIDs WiuiamJames Forresanf're, Englandy Application August 26, 1937,` SerialNo. 160,9)82 In Great-Britain Mayll, 1937 l g, claims. (ci. zio-'452) i f The present invention relates to the filtering and like treatment of liquids with the object of obtaining a pure filtrate. Although the invention is applicable for ltering various liquid ma- 5 terials, it is particularly applicablefor obtaining pure ltrates consisting of viscous liquids containing pigments, powders, crystals or other solid matter in suspension in a finely'divided state. The vpassing of some liquids,A suchas varnishes 10 and oils, through separating-surfaces issometimes termed refining Vandlit is to be understood that the term ltering used herein is intended to cover such treatments and all forms of straining where the object is to. obtain and collect apure liquid filtrate.` Inthewfollowing description the filtering or straining means, which may be gauze (e. g., of metal) silk, cloth, paper, washleather or other material or may bev slots or the like producedby finely/spaced plates orby 2 other suitable means are termedffiltering medium.

The object of the presentk inventionY is toprovide an improved methodof .effecting the filtration, cleaning the filtering vmedium and separating the dross,-i. e., the particles held back by'. the filtering medium, Whilst vavoiding wasteof or-the introduction of foreignk matters Vinto the=liquid being treated andieiecting these objectssofthat the apparatus and filtering 4mediumiis 'protected so far as possible from injury and the; filtration can proceed continuously whilst each portion of the filtering medium` is periodically cleaned in a uniform mannen i i l To eiiect this object I pass the liquid through the filteringY medium and traverse over `the clean side of such medium, i. e., the side on vwhich the filtrate is collected,one or more cleansing heads vtowhicha portion of theliquid is led back under pressure, so .avoiding the introductionof .-air or other foreignmatter which might pollutezor-effeet undesirable changes in the liquid, and allowing the dross to separate itself .from thefliquid under the iniiuenceV of gravity, whilst any moving part which might prejudicially be affectedby the access of the drossisY protected therefrom by the filtering medium.- y v- .i

It is preferred to arrange for the cleaning'action to take place continuously, but insome cases it may be sufficient if thisfisfonlyeiected periodically e. g., if the access-of theliquidto the cleansing heady is interrupted atintervals..v It is however essential that the iilteringqshould proceed continuously,and further thatthe cleansing operation whether continuousV or intermittent should be effected uniformly-so that eaclrpart of the filtering medium is cleaned evenly. I would ftherefore havel itr understood that I do not rinclude in myclaims apparatus in which thecleansing heads consist of movingivanesor other devices `which doy not cleanuniformly each partei" 5 `the filtering medium. a

. vThe liquid can be made to pass through the apparatus byy any convenient means i..e., under the innuence of gravity or by the application of pressure or vacuum.

Anotherobject of the invention is to provide an improved.apparatus for 'carrying out the method. Amongst-other advantages achieved by the invention are, (l) the avoidance of a rotating drum or other filter carrier, since such devices involve 15 the difficult task of maintaining goodY running joints, between the rotating fi1ter`;.drum and itsl end plates creasing, a bad joint or'wear between such.parts-,causingundesirable dross or the like .to lpass into the filtrate; (2) the cleansing head f2.'

works inthevacuum chamber of the filter, viz.,

.the side containing `the filtrate and consequently is free .tomove-Without.hindrance by the presence of dro'ssiwhich isforced bythe pressure in the sectoryolf the filteringniedia on the crudev matev25 rialside of the said media; the entry'of crudev material into the cleaning head is therefore precluded even though a'good kseal'between the head and the filtering media or its support is` not present and furthermore as there is no rejectedfma- 430 terial within the-vacuum chamber, it cannot beA pressed against the filtering surface lby the'movinghead;` (3) there i'sno part which rubs the drossagainst thefiltering media; (4)` lthe arrangement of the movable'head in the yvacuum 135 chamber facilitates the object of allowing the i `,rejected material to settle'by gravity, assisted by the pressureof'the 'cleansing medium, away from 'the filteringzzone;l and (5) a steady and contin-v ruous supply of pressuremedium fori cleaning the -40 filter can `be maintained as the filtering operation proceedsr;

, In order .that the presentinvention may bethe more readily understood, reference `is made to they accompanyingdrawings which show three 45' formsof 4filtering apparatus by way of example -constructed according to the present invention. f Fig. 1 is aside sectional elevation and Fig. 2

an end sectional elevation of one form employing a drum `'type filter and a rotary cleansing heady 50 'l Fig.3 is a side sectional elevation and Fig. v4 a sectional plan of another form employing a disc .type filter anda rotary cleansing head, Fig. 5 .isa section through the cleansing head, looking ,inthe direction of thearrowA, 4. i '55 Fig. 6 is a side sectional elevation and Fig. '7 an end sectional elevation of a third form coinprising a drum type filter and a reciprocating cleansing head.

Fig. 8 is a side View, Fig. 9 an end view and Fig. 10 a plan view of filter and its associated pump and driving motor.

In each of the forms described, the same principle is employed, viz., vacuum and pressure act simultaneously at different zones of the filtering media, preferably without any interruption except for the removal of the rejected material.

According to the first constructional form illustrated, the ltering medium I, e. g., gauze, (e. g., of stainless steel or other metal) silk, cloth, paper, washleather, or any suitable filtering medium is wrapped round a perforated drum 2. The drum is suitably fixed in an outer casing or lreceiver 3 into which the crude or unreiined material is fed, e. g., through a top or side opening or openings 6l, Si, by gravity, pump or any suitable means. It is preferred to cause the material to iiow in quietly by gravity so as to disturb the sludge as little as possible.

This filtering apparatus is particularly applicable for filtering paint, varnish or other material in which the coarse material rejected is heavier than the finer material. Consequently the filteringA drum is arranged in the upper portion of the receiver 3 and the latteris of suflicient depth to enable a gravity separation of the rejected material, so that the latter collects in the bottom of the receiver and is kept clear of the filtering zone and the region in which the cleaning material is forced back to mix with the crude material.V If the sludge were lighter than the liquid the filtering drum would be in the lower portion of the receiving. It is preferred to cause the material to fiow by gravity with as little head as possible, thereby limiting the pressure necessary in .the cleansing head and avoiding too great a return of filtrate through the filtering medium. Moreover in this way the settling by gravitation of the dross forced off the filtering media is facilitated. It is advantageous to run the crude material from a large holder to the filter through a small float-valve controlled tank, so that the head is suitably reduced.V

The receiver conveniently has a tapering sump t into which the coarse material or sludge collects and from which it may be discharged from outlet Ea, conveniently under the controll of a valve l. Within the drum is arrangeda rotating hollow sector ll, the outer faces of which are preferably ground to make a good sliding fit With the internal wall of the drum and/or may be channelled to receive sealing material. The cleansing headmay be in light contact with the filtrate side of the filtering medium or the carrier therefor but in general no absolute contact is necessary. This has the advantage that a space can be left equivalent to the diameter of any fine particles which form part of the filtrate, e. g., particles of 1/1000 inch diameter and thereby wear is avoided and the life of the ltering medium prolonged.

Any substantially greater space should however be avoided as it renders it more'diicult to efficiently clean the medium and to clear the dross away from such medium to a sufficient distance vto facilitate its separation from the liquid land its passage to a portion of the apparatus from which it can be conveniently evacuated.

The sector is mounted'on a hollow shaft 9, the

'interior of which is in communication with the interior ofthe sector, by way of a multiplicity essary where a less viscous material is being if treated so that the ratio of effective filtering area to area under cleaning is reduced, and correspondingly a smaller sector may be desirable for treating more viscous materials. This ratio and the speed of rotation of the sector must in any l5 case be so chosen as to enable the cleansing head to act on any given strip of the filtering medium for a time suiiicient to clean the medium effectively and to enable the cleansing head to reach sufficiently to make it inoperative for ltering. The end plates or discs I2 and the end covers I3a of the casing or receiver are flanged or stepped back at I3b, I3c respectively to form a chamber I4 between each end plate or disc and the corresponding end cover, and the end plates are suitably constructed so that whilst either one of the annular chambers is in constant communication with the interior Illa. of the drum and with the suction side of the external pump I5 by way "S0 of outlet I5 and pipe 49 (Figs. 8-10) and the outlet for the filtrate is not interrupted by the sector-closing portions ofthe end plate I2.

The pump 45 may be a rotary gear pump or oth- N er suitable pump for the purpose of creating a reduction inpressure in the end chamber I4 and in the chamber Ida within the drum so as to assist the fine material to pass through the filtering medium around the drum, whilst the hollow shaft 9 communicating with the interior of the rotating fi'o sector 8 is coupled by means of any suitable coupling or unionxpiece to a pipe I5 leading to the pressure side of the pump. A small percentage of the filtrate is continually bye-passed through the pipe I6 from the pump through the hollow *als shaft and into the rotating sector 8, setting up a pressure in the sector sufficient to overcome the pressure in the receiver 3 containing the incoming crude material. The pressure applied willr depend on the material being treated but in the 50 treatment of certain paints a pressure in the sector of from 5 lbs. to 10 lbs. has been found suitable, depending upon the viscosity of the material.

It is desirable to include a gauge 46 in the line 55 to the sector so that the pressure can be under observation and if desired automatic means may be provided for limiting the pressure when a predetermined reading is reached. The degree of vacuum may also be widely varied. For exam-"lso ple, agauge reading of 1/2 on gauge 4l is generally sulicient in the treatment of paints of somewhat low viscosity, whilst with a paint of rather high viscosity a reading of l0" or over may be reached. 'Ihis gauge 41 may serve as an lfof) indicator, since any undue rise in the reading will indicate that the receiver is accumulating an undesirable quantity of sludge or rejected material. Any undue high vacuum can be overcome/ by returning the greater part of the filtrate to "7U the pressure compartment and through the ltering medium or by closing the discharge valve 48 completely the whole of the filtrate could be returned for a few moments. The sludge or de- A posit meanwhile is removed from the filteringi',

thel same strip again before the latter has clogged T 'medium with immediate decrease in the vacuum.

The discharge valve could be arranged to auto-v -matically close, or partially close, according to the degree of vacuum attained, and the sludge valve could also be automatically opened. Automatic means may be provided for stopping the Ipump or the inflowv of crude material, such means if desired being responsive to the degree of vacuum reached in the filtrate chamber Ma.

The speed of rotation of the sector is also governed by the material under treatment; in

:general the lower the viscosity of the material being filtered the quicker must the pressure sector rotate. When treating paint of a viscosity of `the order of treacle (and specific gravity 2.2), the

running of the sector at about eight revolutions per minute has' given good results. of a specific gravity of 1.5 it was found desirable to double the speed. The sector may be driven With a paint by yan electric motor I] (Figs. 8, 9 and l0) orby ani/ suitable source of power. f

The nature of the filtering medium also has an influence on the pressure with which the material is forced through the filter in one direction and the vacuum for causing the fine material to ,pass through in the first place. vnner gauze it is necessary to employ greater pres- When using a ,sure and a higher degree of vacuum.

During the rotation of the sector the returned filtrate has the effect of blowing or pressing the dross or obstructing material off the filtering surface, forcing it to fall bygravity to the sludge y sump.

Provision may be made to vary the speed of the sector and the speedof the pump. For ex-' ample, expanding pulleys or other variable speed devices may bel interposed in the drive of the "sector and the pump.

'50 or this top opening may merely'serve the function A further lcontainer I8 may be located below .the discharge from the sludge sump. The valve in the sump can be closed whilst the container is being emptied, but otherwise left open, so that the filter need not be stopped for sludge emptying.

It is convenient to provide vinlets 5 for the vcrude material and outlets l5 for the filtrate on opposite sides of the apparatus, the inlet and out'- let on one side being closed, if desired, whilst the others are in use. Or a top opening or openings may be provided for the incoming crude material;

of an air vent. A pressure gauge may be mounted in communication with the receiver.

The hollow shaft carrying the sector vanes maybe removably connected at one end to the driving shaft I9 and at the other end to the aforesaid union piece, appropriate stuffing boxes and glands 20, 2l being provided between'the removable end plates of the casing and the driving shaft'and union piece. v

v The apparatus can be constructed of metal, china, porcelain, wood or any other suitable material, according to the material with which the The invention is not restricted to drum lters.`

According to the constructional form of the in- .vention shown in Figs. 3 to 5, a disc or plate filter A22 is employed. This apparatus may comprise a suitable receiver 3 for the crude material and the lfiltering media 22 and discs 26a, 21 between which it is rclamped divide the receiver into chambers f '23, 24, e. g., upper and lower, the pressure compartment (cleansing head) being in the form of a hollow radial or diametral arm 25 at the end of a hollow shaft 26l which leads the pressure material tothe arm, the latter rotating in the upper 'chamber 23 about the axis of the shaft over the disc of flteringmedia and thereby progressively subjecting zones of the ltering area to cleaning action. The crude material may be fed into the lower chamber 24 preferably at or near the top thereof through inlet 24a so 'as not to disturb 'the sludge and the finer material drawn through the' filtering medium into the upperl chamber,

'whereafter some p-art of the filtrate may be bye- "passed back to the rotating arm, or other pressure medium forced into the arm, and returned through the ltering medium .to mix with lthe crude material. The loWer chamber is of sufficient depth to keep the sludge clear of the filtering medium. f

` The clamping discs 26a, 21 have multipleholes or slots 28 which conveniently are of tapering form enlarging in the direction of the filtering disc so as to present'the maximum filtering area to the material to be treated. The holes in the drum of the drum type could be similarly shaped. l

In certain cases, the` filtering medium could be lstretched. over one perforated plate, the rotating arm moving over the opposite surface of the plate.

The arm may be of uniform cross-section, e. g., .1.. having parallel walls or otherwise but in one. A advantageous form as shown the internal crosssection increases yfrom the axis of rotation to the v vouter end of the arm, (see Fig. 5).

. It is preferred to connect the receiver at 23a to an external pump, but the pump may be located in the receiver and suitably geared,if desired, to

vthe 4rotating arm so that the drive of the latter is derived from the pump shaft. In theY form at present preferred, the arm is .provided with an axial tubular extension 2S passing upwardly through gland 30 in a top cover 3l ofthe receiver `3 and rotating about a fixed `inner tube 32 through which the pressure material lis led to thearm, a suitable gland connection 33 being made between the rotating and the l fixed tubes.A The rotating tube carries a bevel wheel 34 driven by a bevel pinion 35 on a driving shaft 36 varranged over the top of the receiver. A ball or other suitable thrust bearing 3l may be interposed between the rotating arm and tube andthe fixed tube. Adjustment of the pressure arm 25 von the clamping disc 26a is made by actuating-screw 31a and lock nut 31h.

. Neither is it necessary for the purposes of the presentinvention that the pressure compartment should rotate.

Sliding or oscillating devices are equally applicable as for example is shownr in Figs.

A6 and 7. According to this form of the invention,

a filter drum 38 is employed containing a reciprocatingi piston 39 provided with a peripheral groovellll communicating through vhollow spokes ill or the equivalent with a central -hollow shaft 42 which is arranged to be reciprocated to move the piston head to and fro along the drum. Byepassed filtrate or other pressure uid is forced along thehollow shaft and into the peripheral groove, so that as the piston reciprocates the pressure material is forced .through filtering media around the drum into the crude material receiver in which the drumv s'mounted. The

spoked construction of the pistonY head enables the filtrate to pass freely through such head so that the piston has no plunger action, but in reciprocating slowly in the cylindrical drum, the piston merely serves the purpose of conveying the pressure fluid progressively through the filtering medium.

receiver' and filter drum may be similar in Construction to those described in the first constructional form above referred to, the crude material entering at or near the top of the receiver and the filtrate being taken off from within the drum in which the piston reciprccates. The receiver is of sufficient depth to provide space for the material te collect in the lower part of the receiver clear of the filtering media.

According to another variant form a hollow Archimedean screw is employed, the pressure material being conducted to a continuous opening or a series of openings in the outer portion of the screw as such portion works over the inner surface of the drum. l

Any suitable means may be employed for drawing off the filtrate or for feeding the pressure 'duid to the cleaning zone. For example, a devicc werking on the injector principle may be used in place of a pump.

ln some cases two or more filters having filtering media of different mesh could be arranged in the material undergoing graded filtering by first being treated by the coarser mesh media and then by ie finer mesh media.

.nstead of constructing the vacuum chamber, .ie cleansing head and the means for moving the latter as a unit with the crude material receiver, the parts and the filtering'media carried thereby could be partially submerged into a holder for the crude material, the cleansing or pressure head being driven for example by means- Filtering apparatus according to this inventionl may used, as has been previously stated, for a great number of purposes; for example, it could be used in conjunction with the lubricating system of internal combustion or other engines,

e. as part of the lubricating circuit, either on vehicles, ships or elsewhere. It can also be employed in various industries where filtering is necessary, such as in the filtration of beer, and as hereinabove described, paints, varnishes and like viscous materials, or in the filtration of aquecus materials containing solid matter.

Filtration carried out according to my invention presents the following advantages:

The process of filtration proceeds continuouslj. and is not interrupted by the cleansing operation. Tue cleansing head operating on the clean side of the filtering medium and in close proxunity thereto can exert the maximum effect without exposing such ltering medium to the injury which might result if the cleansing head pressed close against it, and further such cleansing head acts uniformly on each part of the filtering medium in turn so that filtration can proceed perfectly evenly. All moving parts to which injury might be caused by the access of dross are protected therefrom by the filtering medium, and since the cleansing is effected by a portion of the filtrate being lead under pressure to the cleansing head no foreign matter is introduced into the liquid being filtered and the dross blown back by the cleansing head separates out from the liquid under the iniiuence of gravity, which avoids the loss of valuable liquid which is involved when such dross is piped away.

We have also found that by projecting the cleansing medium into the main body of the raw material turbulence is produced which apparently assist the regular process of the filtration.

In each of the forms illustrated the cleansing head moves over the clean side of the filtering surface so that the dross is not rubbed against the surface of the filtering medium, since rubbing leads to the breakage of the filtering medium, and we would have it understood that this specification and the claims thereof do not include processes or apparatus in which cleansing heads or Scrapers are applied to the filtering medium on the side on which the dross collects.

It will be observed that in all the forms of construction herein described and claimed, the cleansing means, viz., the cleansing head or heads, the conduit or conduits which convey the filtrate under pressure thereto and the means for rotating the head are conned to the filtrate side of the filtering medium. Such means have no part in the crudematerial and have no connection even by a running joint therewith. Where a running joint is provided extending from one side of the filtering medium to the other, such where the cleansing means comprise a cleansing head on one side and another on the other, the complete isolation of the filtrate from the crude material, except by way of the filtering medium, cannot be obtained since a passage is quickly formed, owing to the wear of the joint, through which crude material can pass and mix with the filtrate. By the method according to the present invention the filtrate is completely isolated from the crude material, except by way of the filtering medium, since there are no joints to which the crude material can obtain access.

What I claim is:

l. A method of filtering solid bodies out of liquids to obtain a pure filtrate which consists n passing the liquid to be filtered through a stationary filtering medium, isolating the filtrated liquid completely from the crude material except by way of the filtering medium, returning a coni fined body of the filtrate toward the filtering medium under a pressure greater than that of the crude material and passing said confined body of nitrate under pressure through a portion of the filtering medium in a direction reverse to the main new therethrough to dislodge the dross adhering to the crude material side thereof and to discharge same together with the returning fil-- trate into the crude material whilst continuously carrying on filtration, moving said confined body of filtrate under pressure progressively over the filtrate side of the filtering medium and maintaining its volume uniform so that the crude material side of the filtering medium isuniformly cleansed, said returning filtrate carrying the k dross therewith freely mixing with the crude materal whereupon such dross or the major portion thereof separates itself from the crude material under the influence of gravity.

2. A method of filtering solid bodies out of lio iii

, liquids to obtain a pure filtrate, comprising aV liquids to obtain a pure nitrate which eonsisi-sA in passing the liquid to be filtered through a sta- 1 tionary filtering medium under the infiuence of a vacuum, isolating the crude material completely from the filtrated liquid except, by way of thev filtering medium, returning a confined body of thecrude material whilst continuously carrying on filtration, continuously moving s aid confined bodyof filtrate under pressure progressively over the filtrate side of the filtering medium and maintaining its volume constant so that the crude material side of the filtering medium is uniformly cleansed, said returning filtrate carrying the' dross therewith freely mixing with the crude. material whereupon such dross or the major portion thereof separates itself from the crude material under the influence of gravity.

3. Apparatus for filtering solid bodies out of receptacle, an inlet thereto for the crude material to be filtered and an outlet therefrom for f` the dross, a filtrate chamber ywithin said receptacle, filtering means within said receptacle completely separating the filtratechamber from said inlet, said filtering means being fixed in re- Vliquids to obtain a pure filtrate, comprising a receptacle, an inlet thereto for the crude material to be filtered and 'an' outlet therefrom fon lation to said filtrate chamber, means for pass- .ing the liquid to be filtered through said filtering means into said filtrate chamber, cleansing means for said filtering means consisting of at least one movable cleansing head arranged in `said filtrate chamber with its opening in close' proximity to said ltering means so as to form n therewith a cleansing chamber whichr is substantially closed from the filtrate chamber and confined wholly to the filtrate side of said filtering means so that such cleansing means have no "part in the crude material receptacle and no communication even by a running joint therewith except through said filtering means; saidy I cleansing means alsoincluding a conduit` for conveying filtrate under pressure to said head; means for moving said head in said filtrate chamber over the filtrate side of said filtering means; and` means for forcing a'portionof tlieltrated liquid under pressure through said conduit to said cleansing head and thence through a portionl of the filtering means todislodge dross adhering to the receptacle side of the filtering means and to discharge same together with the dross carrying filtrate into said receptacle whereupon the drossforced off of the filtering means separates by gravity from the liquid being filtered and accumulates in the receptacle away from the filtering means.

4. Apparatusfor filtering solidbodies out of liquids to obtain ia pure filtrate, comprising a receptacle, an inlet thereto for thecrude lmaterial to be filtered and. an outlet therefrom' for the dross, filtering means fixed inl said receptacle dividing the same into a receiving chamber and an upper filtrate chamber; a pump for creating a partial vacuum in said filtrate chamber to draw y the liquid fromr thefreceiving ,chamber through the filtering means,l cleansing means in saidv Ife-k ceptacleand confined to the filtrate side of said filtering'means so that such cleansing means have no part in the crude material receptacle'and no communication even by a running joint theref with'except through said filtering means, said kcleansing means consisting of at least one movable cleansing' head positioned in close proximityy to the said filtering means so as to form therewith a cleansing chamber whicliis substantially closed 'from the filtrate chamber, ofA at least one conduit for` conveyingfiltrate under pressure to said', head and of-,means formoving said head invsaid filtrate chamber over the filtrate side of Vsaid filtering means; and liquid connections between said pump and cleansing head for forcing part of the filtrate drawn through the filtering means -under pressurethrough saidconduit to said cleansing-head, a funnel-like sump underlying vsaid filtering means and 'located in the lower part of said' receiving chamber for receiving the dross forced off the filtering means as it separates by gravity from the liquid to be filtered;

5. Apparatus for filtering solid bodies out of the dross, a stationary filtering drum,mounted in the upper part of saidl receptacle forming a. filtrate chamber,l a rotatable hollow sector arranged-in said chamber in closeproximity to the filtrate side yof said filtering drum so as to form therewith a cleansing chamber which is substantially closed from the filtrate chamber, meansr for rotating saidv sector in saidfiltrate chamber over the filtrate side of said filtering means, said means in a direction reverse to the main fiow through said filtering means for dislodging the dross-adhering to the receptacle side of said filteringmeans and to discharge samer together with the returning filtrate into said receptacle f wherein it separates by vgravity and accumulates in thelower portion of the receptacle away from the 'filtering medium.

JAMES FORREST. 

